|Número de publicación||US4610801 A|
|Tipo de publicación||Concesión|
|Número de solicitud||US 06/790,632|
|Fecha de publicación||9 Sep 1986|
|Fecha de presentación||22 Oct 1985|
|Fecha de prioridad||24 Sep 1982|
|También publicado como||CA1216781A, CA1216781A1, DE3371196D1, EP0104904A1, EP0104904B1, US4711727, WO1984001145A1|
|Número de publicación||06790632, 790632, US 4610801 A, US 4610801A, US-A-4610801, US4610801 A, US4610801A|
|Inventores||Kenneth B. Matthews, Christine A. Beckett, David E. Smith, Richard R. Davidson|
|Cesionario original||Blue Circle Industries Plc|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (22), Citada por (69), Clasificaciones (19), Eventos legales (4)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
This application is a continuation of application Ser. No. 534,561, filed Sept. 22, 1983, now abandoned.
This invention relates to compositions comprising an aqueous suspension of mineral particles of high solids content.
It also relates to a method of treating an aqueous system with such a composition, optionally after dilution of the latter. Thus, for example, the method may be applied to the flocculation/coagulation of sewage or other waste water, or to the incorporation of flocculated filler in papermaking stock.
Particulate minerals are useful in the treatment of sewage as they aid the clarification of waste water in, for example, conventional sedimentation processes, especially at the primary sedimentation stage. Thus, lime is well known as a coagulant in sewage sedimentation and in sludge conditioning prior to filtration. Lime is often used with the separate addition of other flocculants/coagulants, e.g. high molecular weight cationic polyacrylamides, ferric chloride, ferrous sulphate or alum.
This lime is normally used as a powder or as a dilute (say 10% solids) slurry prepared, for instance, by slaking on site. However, this requires plant to handle powdered lime or to slake quicklime; furthermore, powdered lime is an unpleasant material to work with. Moreover, the separate addition to the aqueous system of lime and other additives creates problems on site with handling, proportioning and metering.
Other particulate minerals, such as calcium carbonate are useful in sewage treatment, for example, as weighting agents. A mixture of hydrated lime and calcium carbonate can be particularly useful, as described in United Kingdom Patent Specification No. 2,095,226.
In papermaking, mineral particles such as calcium carbonate are used as fillers and pigments. The use of flocculated mineral particles is advantageous in that it allows higher than usual filler-loading levels to be achieved without loss of paper strength (see, for example, the discussion in U.K. Patent Specification No. 2,016,498). The flocculant may be added separately to the papermaking stock, before or after the filler is added as a slurry.
As an alternative to separate addition, both in sewage or other waste-water treatment and in papermaking, the flocculant may be added to a slurry of the mineral particles immediately before use. This requires special plant to ensure good mixing of the components and to ensure that the resultant suspension is conveyed immediately to the point of use. There are severe difficulties, however, in incorporating conventional flocculants into higher solids content slurries as they cause gross flocculation and thickening such that the resultant slurry does not flow readily and is not readily pumpable except with special equipment.
It would clearly be desirable to provide suspensions of mineral particles having a high solids content that are readily and economically transportable, especially such suspensions that contain the other components required to carry out the desired coagulation/flocculation process. Such suspensions could be manufactured with consistent quality and they would simplify on-site dosage and application, being a `one-pack` product. Thus, they could obviate or reduce the need for expensive plant on site to handle powders, liquids or slurries, to proportion and meter components added separately or to mix particle suspensions and a flocculant at high speed. Furthermore, the higher the solids content, the greater is the reduction in the costs entailed in transporting water.
However, to be practicable, such suspensions of high solids content would have to be simple to handle and apply, and be readily pumped/metered at controlled rates. Here, two problems must be overcome. Firstly, the viscosity characteristics of high solids slurries deteriorate rapidly as their solids content is increased. For example, for a lime slurry with no additives and having a solids content of 50% by weight, the following measurements have been made: a yield of 1335 dynes/cm2 and an apparent viscosity at 600 s-1 shear rate of 264 cP (measurements made on a Haake Rotovisco RV2 viscometer using cup MV St and bob MVI).
Some reduction in viscosity can be achieved by the incorporation of a small amount of a dispersing or surface-active agent such as a polyphosphate, a salt of a polyacrylic acid or a salt of polymethacrylic acid. The latter two are preferred in water/sewage treatment. The use of these materials alone, however, generally leads to the production of a stubborn sediment on settling.
Secondly, the addition of a flocculant to a mineral suspension normally causes heavy flocculation of the particles and results in a thick paste which is difficult to handle in processing plant, slurry tankers, and the like.
The present invention now provides a composition for treating an aqueous system, which composition comprises (a) an aqueous slurry of mineral particles of at least 40% m/m mineral solids concentration and (b) an agent that at least substantially maintains the mobility of the slurry (a) and that exerts a flocculating action upon addition of the composition to an aqueous system at a dilution ratio of at least 20:1 (m/m).
The invention makes possible the formulation of self-flocculating, non-settling, pumpable, transportable "total" slurries, i.e. slurries which contain all the components necessary to effect the required coagulation/flocculation process. The component (b) in the slurry can be activated by simply diluting the slurry at the point of application with or into either water or the aqueous liquid of the system to be treated, whereupon it will enhance any flocculating action exerted by the mineral particulate matter. Looked at another way, the component (b) will cause an increase in the flocculation of the mineral particles upon dilution to a low solids content.
Accordingly, the present invention also provides a method of treating an aqueous system, in which there is applied to said system a composition of the present invention, said composition being applied as such or after dilution.
The mobility of the slurry is deemed to be maintained if the apparent viscosity of the slurry (as measured on a Haake Rotovisco RV2 viscometer at a shear rate of 600 s-1) is not above 500 cP. In the case of lime-containing slurries it is desirable that the apparent viscosity should not exceed 300 cP. For all compositions of this invention, the apparent viscosity is preferably below 200 cP. In order to obtain acceptable pumpability, the slurry preferably exhibits a plastic viscosity of not more than 150 cP, especially not more than 100 cP, and a yield stress of not more than 600 dynes/cm2. Normally the yield stress will not be below 50 dynes/cm2 and is preferably from 50 to 300 dynes/cm2.
By "self-flocculating" we mean that the composition forms flocs of particlate matter on dilution with or into water (at least a 20:1 (m/m) dilution). The water may be soft water, hard water or water that has been hardened by the addition of one or more salts of multivalent cations (e.g. Ca2+, Mg2+ or Al3+) although the effects are better in hard or hardened water. In general, the water will contain dissolved salts equivalent to at least 50 ppm calcium hardness and typically up to 500 ppm. The water can also be the aqueous component of a system to be treated, such as sewage or a papermaking stock, which two systems usually contain suspended particulate matter of an anionic character. In such cases the formation of co-flocs of mineral particles from the slurry and particulate matter from the aqueous system being treated is comprehended within the method of this invention.
A "non-settling" slurry is one which exhibits acceptable stability and therefore a reasonable shelf life. To be of practical use a slurry must have an acceptable shelf life which in terms of these slurries is a resistance to the formation of a hard sediment on standing. An acceptable slurry may slowly settle to form a supernate and a sediment but the sediment must be readily redispersed on agitation (e.g. slow-speed sweep agitation) after at least 3, and preferably after at least 7, days' settlement.
The mineral particles can be of a single material or a mixture of materials. Preferred materials are the oxides, hydroxides, sulphates, carbonates and bicarbonates of the alkaline earth metals; especially preferred are calcium carbonate (in any form, for example limestone, whiting or precipitated chalk), calcium hydroxide and mixtures of these two (preferably mixtures with a weight ratio of from 19:1 to 1:19 and especially from 5:2 to 2:5). Other mineral fillers are also possible, such as calcium sulphate (e.g. gypsum), talc, clay, titanium dioxide, zinc oxide, lithopone, barium sulphate, kaolin or zinc sulphide. Useful sources of calcareous particulate minerals include waste materials from a cement works, e.g. flue dust, and waste materials from a lime works, lime softening process or desulphurisation process.
Although preferred compositions contain calcium carbonate, it is possible to use barium compounds as a partial replacement for the carbonate. The barium compounds, owing to their weight, may improve the settling of the sewage or other particulate waste to be treated.
Some calcium carbonates that occur naturally with an alumino-siliceous surface layer, or calcium carbonates so modified, may be of particular advantage in this invention.
The component (b) that at least maintains the mobility of the slurry will contribute to the required coagulation/flocculation process when the composition is applied to the aqueous system to be treated. One class of preferred agents are cationic polyelectrolytes having nitrogen-containing groups (e.g. quaternary nitrogen-containing groups), e.g. polyamines (including the quaternary polyamines), polyimines and dimethyl diallyl ammonium chloride polymers.
One group of such polyelectrolytes, which are especially suitable for the treatment of sewage, are those with a low molecular weight (in particular 106 or less) and high change density; in papermaking, such polyelectrolytes of higher molecular weight may also be suitable.
Amphoteric polyelectrolytes, e.g. those having nitrogen-containing groups (e.g. quaternary nitrogen-containing groups), may also be useful herein.
Especially preferred for sewage treatment are quaternary polyamines, e.g. those available under the trade names Magnafloc 1597 (from Allied Colloids) and Accurac 41, Superfloc C573 and Accostrength 711 (from American Cyanamid); dimethyl diallyl ammonium chloride (DMDAAC) homopolymers, e.g. those with molecular weights of from 30,000 to 106, such as those available under the trade names Catfloc, Catfloc T and Catfloc T-1 (from Chemviron); and especially preferred for papermaking are DMDAAC/acrylamide co-polymers, e.g. those available in solution or emulsion form under the trade names WT 2860, WT 2640, WT 2575, WT 2635 and WT 5504 (from Chemviron).
Polyethylene imines, such as those available under the trade name Polymin (from BASF), may also be used.
Generally, it has been found that the cationic and amphoteric agents described above for component (b) do not merely maintain the mobility of the slurry but actually increase it at any given concentration of mineral particles.
Provided that the composition contains calcium hydroxide the component (b) may also be selected from anionic polymers, especially the anionic polyacrylamides, and more especially such polyacrylamides of high molecular weight, e.g. those available under the trade marks Magnafloc 155 and Magnafloc 156.
Component (b) may be present in the composition in an amount of, in general, from 0.0075 to 2%, preferably from 0.01 to 1.0%, on a dry weight basis.
The substances mentioned above as being suitable as component (b) are generally regarded as flocculants; it is therefore surprising that they can be used in accordance with the present invention to prepare mobile slurries or suspensions of high solids content.
The compositions of this invention may, of course, contain other components. For example (c) a structure-modifying agent (structuring aid) may be included, if appropriate. Synthetic hectorite has proved suitable for this purpose.
The structure-modifying agent (c) may be present in the composition in an amount of, in general, from 0.005 to 0.5%, preferably from 0.01 to 0.1% on a dry weight basis.
The composition of this invention may be prepared by initially forming an aqueous slurry of mineral particles in the presence of (d) a dispersant and then adding the component (b). Other methods of preparation may, of course, be employed, for example the dispersant may be included in the particulate mineral starting material and the component (b) may be added stepwise during the formation of the slurry.
Suitable dispersants are polyphosphoric acids, polyacrylic acid, polymethacrylic acid and their salts, as well as lignosulphonates and the like. The dispersant (d) may be present in the composition of this invention in an amount of, in general, from 0.005 to 2%, preferably from 0.01 to 0.5%, on a dry weight basis.
Of course, each component (b), (c) and (d) can be a mixture of suitable materials.
In order to improve the efficiency of the treatment of sewage with a composition of the present invention, especially with a preferred composition that contains a mixture of lime and calcium carbonate as the mineral component, it is possible to use one or more auxiliary agents selected from known flocculants, such as sodium aluminate, ferric sulphate, ferrous sulphate, aluminium chlorohydrate, polyelectrolytes or, preferably, aluminium sulphate (papermakers' alum). Although it is possible to include the auxiliary flocculant entirely in the present composition, it is preferred to add some or, preferably, all of the auxiliary flocculant to the sewage in a separate addition step after the addition of the present composition. Such a separate addition can settle the light, loose flocs that occasionally break away from the main flocs or it can improve the characteristics of the originally formed flocs in order to improve settlement. It is, however, also possible to add the present composition (or "total slurry") in steps.
The mixing regime, in particular the level of shear and the period for which the additives are left in contact with the system being treated, can influence the efficiency of the process of the present invention. However, suitable conditions can be determined in any given situation.
As mentioned in No. GB-A-2095266 (page 1, line 49 to page 2, line 9) various types of apparatus are used for the settling and clarification processes in the treatment of sewage, including static settling tanks (which may be coupled to a flocculation unit), sludge-blanket clarifiers, and the "once-through" plant developed by P. Stead and B. Winfield for the rapid sedimentation of primary sewage. The present compositions can be used with these and other apparatuses, as well as with an hydraulic separating device, e.g. the separator described in No. GB-A-2,082,941.
The compositions of this invention find particular use in the treatment of sewage and in papermaking (although the lime-containing compositions are usually inappropriate for the latter). Further applications for these slurries include use in water treatment (e.g. the softening of water), in the treatment of waste effluents, e.g. from pigs, abattoirs and heavy-metals industry, and for the desulphurisation of gases, for example in wet scrubbers and the like.
The optimum amount of the "total slurry" to be used in the process of the invention will depend on the nature of the aqueous system to be treated and the conditions under which the addition is to be made. Commonly, it will be appropriate to employ a dosage rate of 100 to 1,000 ppm, typically from 200 to 500 ppm, on a dry mineral basis relative to the total aqueous system to be treated.
In the following Examples, the components were selected from the following materials.
Northern or Sourthern (English) chalk whitings in powder, high solids slurry or filter-cake form. Hydralime (hydrated lime; from Blue Circle Industries).
Tetron (tetrasodium pyrophosphate; from Albright & Wilson).
Dispex N40 (sodium polyacrylate; from Allied Colloids).
Laponite RD (synthetic hectorite; from Laporte).
WT 2575 (DMDAAC/acrylamide copolymer in solution form; high molecular weight, cationic).
WT 5504 (DMDAAC/acrylamide copolymer in emulsion form; amphoteric).
Magnafloc 1597 (a quaternary polyamine; molecular weight about 5×105 ; about 50% active as marketed).
Magnafloc 155 or 156 (high-molecular-weight (ca. 5×106) anionic polyacrylamides; anionic character 20%).
Catfloc T-1 (a DMDAAC homopolymer).
Accurac 41 (a quaternary polyamine).
Superfloc C573 (a quaternary polyamine).
Colour Improvement Agent:
Sodium hypochlorite solution (15% available chlorine).
All viscosity measurements were effected using a Haake Rotoviscon RV2 viscometer at a shear rate of 600 s-1. Except where stated otherwise, the slurries of this invention described in the Examples were non-settling, as defined above.
Examples 1 to 4 describe compositions that would be suitable for use in the preparation of paper fillers.
The following formulation was prepared:
52.6 kg water
256.8 kg 73.6% m/m Southern whiting filter cake
519.7 g Tetron
75.6 g Laponite RD
945 ml sodium hypochlorite solution
4.7 kg WT 2575
The dispersant and structure modifier were added simultaneously under high shear to a slurry of the whiting in the water. Sodium hypochlorite solution was added under high shear, followed by the flocculant under just sufficient shear to produce a homogeneous total slurry of 60% m/m solids content. Apparent viscosity 259 cP; yield 557 dynes/cm2.
This total slurry was used in the preparation of laboratory paper handsheets, whereby the undiluted total slurry was pumped into papermaking pulp thin stock, thereby diluting the slurry by a factor of from 120:1 to 270:1, depending on the level of filler loading, whereupon the slurry solids flocculated. A high-solids whiting slurry was used in laboratory hand-sheet preparation under identical conditions to provide a comparison for the performance of the total slurry. Advantages of the use of total slurry in terms of filler retention and paper strength were evident in the results:
TABLE 1______________________________________% Whiting retained Burst Strength Tensile Strengthon Handsheet (Burst Ratio) (Breaking Length)Whiting Total Whiting Total Whiting TotalSlurry Slurry Slurry Slurry Slurry Slurry______________________________________5.7 9.1 3.96 4.17 6525 69698.0 12.3 3.56 4.07 6135 658211.8 15.9 3.07 3.72 5579 6264______________________________________
1042.5 g 70% m/m solids, colour-improved whiting slurry
1.569 g Tetron
157.8 g water
18.25 g WT 2575
The dispersant was added to the whiting slurry (which contained a small quantity of Laponite RD) under high shear, followed by the water and flocculant under low shear to give a 60% m/m total slurry. This order of addition ensured maximum efficiency of use of the dispersant by dissolution in the maximum solids content whiting slurry. Apparent viscosity 350 cP; Yield 440 dynes/cm2.
The pumpable total slurry could be used to prepare flocculated filler by dilution into a papermaking thin stock, as described in Example 1.
500 g 73.6% whiting filter cake
64.2 ml water
0.29 g Tetron
0.15 g Laponite RD
1.84 ml sodium hypochlorite solution
0.92 g WT 5504
A method of preparation similar to that of Example 1 was used to give a 65% total slurry, which was stable to hard-sediment formation for 11 days and more. Apparent viscosity 129.6 cP; yield 176 dynes/cm2.
The pumpable total slurry could be used to prepare flocculated filler by dilution into a papermaking thin stock, as described in Example 1.
The following formulation was prepared.
______________________________________Deionised water 100 gSnowcal 6ML, natural chalk whiting 194 g(from Blue Circle Industries)The whiting was added in portions to thewater while stirring with a laboratory propellerstirrer. The mixture was thick, "short" andwas not circulated by the stirrer, and ondilution with deionised water formed shear-reversible flocs. There was then addedAccurac 41 0.67 gThe mixture thinned at once and wascirculated by the stirrer indicating at leastpartial deflocculation of the particles. Itwas now possible to add:Snowcal 6ML 40.0 gThere was some thickening, and there wasfurther added:Accurac 41 0.5 g 335.17 g______________________________________
The resulting suspension had a content of whiting of 69.8% w/w. It had a pumpable viscosity. Flocculation would occur on addition to anionic paper stock. The suspension showed no hard sedimentation after 1 month's storage. During this time there was a slight thickening and an increase in the gel-structure present initially; this structure was presumably responsible for the resistance to hard sedimentation.
In passing, it may be mentioned that the degree of flocculation of dilute particle suspensions may semiquantitively be assessed by observing the rate of sedimentation in a beaker, and the clarity of the supernatent liquid. It is also valuable to observe a pool of a suspension of white particles kept in gentle motion on a black surface. Floc formation can in this way be observed by eye. The flocs may be broken down to an extent by rubbing with a finger, and reflocculation, if present, observed.
The following Examples 5-12 describe compositions that would be suitable as coagulant/flocculant additives in sewage treatment.
(a) A lime/carbonate slurry was made up as follows using calcium carbonate in slurry form:
42.5% m/m solids whiting slurry (Snowcal 20SW; from Blue Circle Industries): 300 g
Hydralime: 127.5 g
Water (mains): 82.5 g
This slurry had the following viscosity figures: yield 484 dynes/cm2 ; apparent viscosity 120 cP.
(b) Magnafloc 1597 (0.05% on a dry weight basis) was then added to the above slurry and mixed in a high speed disperser. The resultant slurry had the following viscosity figures: yield 161 dynes/cm2 ; apparent viscosity 54 cP.
The clarification of sewage on settlement could be improved by the flocculation of the gross and colloidal suspended matter using the slurry. The efficiency of the slurry in treating sewage was shown firstly in the laboratory using a conventional "jar test" (see J. Bratby, "Coagulation and Flocculation", 1980, Uplands Press Limited, Chapter 8, pp 265-266 and 271-272) with the following stirring regime: 30 seconds' fast mixing, 5 minutes' slow stirring and 15 minutes' settlement time before withdrawing a sample for tests on turbidity, pH and suspended solids content. The following results were obtained:
TABLE 2______________________________________"Total Slurry" Suspended TurbidityDose mg/l Solids mg/l NTU pH______________________________________ 0 275 275 7.7200 94 80 8.5400 48 32 9.5600 26 20 9.9800 23 14 10.7______________________________________ (NTU = nephelometric turbidity units).
The effect of predilution was also investigated. For example, in sewage treatment using a 437 mg/l dose of the total slurry of Example 5(b), the following results were obtained:
TABLE 3______________________________________ Turbidity (NTU)______________________________________Crude sewage 200No predilution 575:1 predilution of slurry 5410:1 predilution of slurry 5320:1 predilution of slurry 3850:1 predilution of slurry 24100:1 predilution of slurry 14______________________________________
A predilution with water of 20:1 or more is beneficial. However the water in the aqueous sewage, papermaking or other system being dosed can provide a suitable level of dilution to effect flocculation.
The effect of different shear regimes was also investigated by prediluting the total slurry of Example 5(b) and then adding the diluted composition to sewage in a conventional jar test during a period of rapid mixing. The treated sewage was then subjected to a period of slow mixing following which the turbidity was measured. The results are summarised in the following table.
TABLE 4______________________________________Addition of2.5% m/m TS TS Rapid Mixing Slow Mixing(g) (ppm) Time (secs.) Time (mins.) NTU______________________________________8 400 5 2.5 718 400 15 2.5 658 400 20 2.5 588 400 30 2.5 588 400 40 2.5 428 400 30 5.0 40/418 400 30 15.0 33______________________________________ Notes: TS = total slurry NTU = turbidity = nephelometric turbidity units.
At a conventional sewage works the following results were achieved at the primary stage. A 50% m/m total slurry prepared according to Example 5(b) was prediluted by at least 20:1 with water (pressurised returned effluent could have been used) immediately before addition to one half of the influent screened sewage. Good mixing occurred as the sewage passed over a weir into the first distribution chamber on passage to one of two primary sedimentation tanks. The remaining half of the influent screened sewage passed untreated to the second primary sedimentation tank as a control.
TABLE 5______________________________________ Crude Untreated Treated Sewage Settled Settled (Mean Sewage SewageParameter Values) (Mean Values) (Mean Values)______________________________________Suspended 334 159 102Solids (mg/l)Turbidity (NTU) 315 168 67E. coli 1.24 1.12 0.16(No. × 10.sup.7 /100 ml)BOD.sub.5 (mg/l) 208 -- 97Phosphate (mg/l) 10.5 10.6 2.0______________________________________
(a) A 50% m/m lime/carbonate slurry was prepared as in Example 5(a). Yield 425 dynes/cm2 ; apparent viscosity 104 cP.
(b) After addition of 0.05% Catfloc T-1, in a high speed disperser, a slurry was obtained having the following figures: yield 161 dynes/cm2 ; apparent viscosity 59 cP. This sample exhibited suitable flocculation characteristics. This slurry was added to sewage from Longreach, Dartford, England, in a conventional "jar test". The following results were obtained:
TABLE 6______________________________________Total-slurry Turbiditydose (ppm) (NTU) pH______________________________________ 0 283 7.8200 78 8.6400 43 9.1600 26 9.4800 20 9.7______________________________________
(a) A number of jar tests were carried out in which sewage was treated by the addition of a total slurry according to the present invention and prepared as described in Example 5(b). The treated sewage was then further treated by the addition of either ferric sulphate or aluminium sulphate (alum), these being representative of the conventional flocculants used in the treatment of sewage. The turbidity of the sewage treated in the aforesaid manner was compared with the turbidity of the sewage treated with the total slurry alone. The results are given in the following table:
TABLE 7______________________________________Flocculant TS NTU (TS + NTU (TS Improvementppm ppm flocculant) alone) (%)______________________________________Ferric 200 26 40 +35sulphate40Alum40 100 18 79 +77.240 200 13 40 +67.540 500 11 28 +60.7______________________________________ Notes: TS = total slurry NTU = turbidity measured in nephelometric turbidity units.
Improvement was calculated using the formula
A=NTU obtained with total slurry alone
B=NTU obtained with total slurry and subsequent addition of the conventional flocculant.
(b) Two further series of jar tests were carried out in which sewage was treated with a total slurry prepared as described in Example 5(b) and with alum. In one series, the entire dose of alum was added subsequently to the addition of the total slurry; in the other series, a proportion of the alum was included in the total slurry itself, the remainder of the alum being added to the sewage after the alum-containing total slurry had been added.
Control tests were carried out in which only an alum-free total slurry was added to the sewage. The turbidity (in NTU) and the pH of the treated sewage were measured in each test and the results are given below:
TABLE 8______________________________________Total Alum added Alum addedSlurry with total separately(ppp) slurry (ppm) (ppm) NTU pH______________________________________100 5 35 23 7.9100 0 40 18 7.9100 0 0 79 8.0200 10 30 38 8.3200 0 40 28 8.3200 0 0 58 8.5500 25 15 21 8.9500 0 40 11 9.0500 0 0 28 9.0______________________________________
These and other tests have indicated that improvements in the clarification efficiency of the lime/carbonate total slurry treatment process can be gained by the separate addition of a conventional flocculant to the sewage after the total slurry has been added. Alum has given the largest increase in efficiency.
The optimum level of addition of the auxiliary flocculant will obviously depend upon the nature of the sewage and will have to be determined at any given site. However, the cost of the separate addition of alum may be offset by the possibility of reducing the dosage level of the total slurry. For example, as indicated in Table 8, an addition level of 500 ppm total slurry alone gave a turbidity of 28 NTU, whereas the same turbidity could be achieved by the addition of only 200 ppm total slurry in conjunction with a subsequent addition of 40 ppm alum.
Although, as indicated above, it would be feasible to incorporate the auxiliary flocculant, wholly or partly, into the total slurry, it has been found that any improvements in clarification efficiency are not cost effective.
The slurry of Example 5(b) was used as the flocculant in an upward flow sludge blanket unit treating domestic sewage. The flocculant slurry was metered from the supply tank at 400 ppm (dry basis) on sewage flow ratio, and was continuously diluted with mains water at the 40:1 level. The preflocculated slurry was then added to the influent crude sewage. Good flocculation of the suspended matter was achieved and a sludge or floc blanket readily formed in the unit. The quality of the effluent which discharged from the top of the unit was compared with the influent sewage and good clarification was evident when the sewage flow through the upward flow sludge blanket was at a 1 l/s/m2 surface loading level.
______________________________________Results:Raw Sewage EffluentSuspended solids Suspended solids Turbiditymg/l pH mg/l pH (NTU)______________________________________350 8.1 58 9.1 50______________________________________
A slurry was prepared as follows:
______________________________________Snowcal 4ML (chalk whiting; from 50 gBlue Circle Industries)Deionised water 50 gHydrated lime 50 gDeionised water 20 g(The resultant mixture was a slip-pasteof 59% solids content)Accurac 41 0.5 g(There was an increase in the flowindicating some deflocculation)Superfloc C573 flocculant 1.0 g 171.5 g______________________________________
A composition of acceptable flow and stability properties was obtained.
When high molecular weight, cationic polyacrylamides typically used in sewage treatment (e.g. Zetag 92, Zetag 51; from Allied Colloids) are added to a lime/carbonate slurry, heavy flocculation occurs such that the slurries become too thick to pump. The following formulation was prepared.
Snowcal 20SW (42.5% m/m): 300 g
Hydralime: 127.5 g
Water: 82.5 g
Zetag 92 (0.04% on dry solids): 0.1 g
The resultant slurry had the following viscosity properties: no yield value as such (pseudoplastic); apprarent viscosity (at 600 sec-1) 386 cP.
Snowcal 20SW: 300 g
Hydralime: 127.5 g
Water (mains): 82.5 g
Magnafloc 156 (0.0125% on a dry weight basis) was then added. The resultant slurry had an apparent viscosity of 114 cP and a yield value of 393 dynes/cm2, and produced very coarse flocs on dilution.
The following formulation was prepared
______________________________________Hydrated lime 50.0 gDeionised water 60.0 g10% sodium hydroxide solution 2.0 gSnowcal 3ML (calcium carbonate) 50.0 g50% Dispex N40, 50% Accurac 41 1.5 g0.28% Zetag 92 solution containing 10.0 g2.0% of sodium hydroxide 173.5 g______________________________________
This sample was prepared by hand stirring and showed freedom from sedimentation and a tendency to become thinner on standing. Flocculation in hard water was extremely good.
The following formulation was prepared:
______________________________________Hydrated lime 100 gDeionised water 90 g2% caustic soda solution 4 g5% Dispex N40/Accurac 41 4.7 g0.28% Zetag 92, 0.28% caustic soda 10.0 gsolution 208.7 g______________________________________
This was just pumpable at 50% solids content but thinned considerably on standing. The apparent viscosity was 95 cP and the yield stress 88 dynes/cm2. Flocculation in tap-water was extreme.
As can be seen from the two foregoing Examples, it is possible to incorporate a cationic, high-molecular-weight polyelectrolyte such as a polyacrylamide (normally a bridging flocculant for mineral particles) into the compositions of the present invention, especially those that contain a cationic low-molecular-weight polyelectrolyte as the component (b).
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3892587 *||17 Jun 1974||1 Jul 1975||Huber Corp J M||Method for controlling the viscosity of dispersed clay slurries|
|US3961979 *||17 Jun 1974||8 Jun 1976||J. M. Huber Corporation||Method for controlling the viscosity of dispersed clay slurries|
|US3994806 *||8 Mar 1972||30 Nov 1976||Calgon Corporation||Composition and method for flocculating suspended solids|
|US4024087 *||6 Nov 1975||17 May 1977||Jury Abramovich Lainer||Method of preparing coagulant for purification of water from mechanical admixtures|
|US4402851 *||8 Ene 1982||6 Sep 1983||Boliden Aktiebolag||Pumpable composition for water-purifying purpose containing iron (II) sulphate, and a method for producing the same|
|US4450092 *||11 Jun 1982||22 May 1984||Nalco Chemical Company||Reducing turbidity in turbid waters|
|DE3004611A1 *||8 Feb 1980||13 Ago 1981||Hoechst Ag||Hochkonzentrierte fuellstoffslurries|
|GB845838A *||Título no disponible|
|GB870711A *||Título no disponible|
|GB1159819A *||Título no disponible|
|GB1214532A *||Título no disponible|
|GB1230166A *||Título no disponible|
|GB1312751A *||Título no disponible|
|GB1497280A *||Título no disponible|
|GB1527304A *||Título no disponible|
|GB1583881A *||Título no disponible|
|GB1588016A *||Título no disponible|
|GB2004535A *||Título no disponible|
|GB2016498A *||Título no disponible|
|GB2095226A *||Título no disponible|
|GB2134508A *||Título no disponible|
|JPS57184430A *||Título no disponible|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US4711727 *||29 Jul 1986||8 Dic 1987||Blue Circle Industries, Plc||Compositions comprising mineral particles in suspension and method of treating aqueous systems therewith|
|US4732748 *||10 Dic 1986||22 Mar 1988||Cyprus Mines Corporation||Finely divided calcium carbonate compositions|
|US4746457 *||5 Mar 1987||24 May 1988||Calgon Corporation||Flocculation of suspended solids from aqueous solutions|
|US4800039 *||5 Mar 1987||24 Ene 1989||Calgon Corporation||Flocculation of suspended solids from aqueous solutions|
|US4874466 *||28 Sep 1988||17 Oct 1989||Nalco Chemical Company||Paper making filler composition and method|
|US5017268 *||2 Sep 1987||21 May 1991||E. I. Du Pont De Nemours And Company||Filler compositions and their use in papermaking|
|US5061461 *||22 Ago 1990||29 Oct 1991||Engelhard Corporation||Cationic processing of kaolin ores|
|US5071587 *||31 May 1990||10 Dic 1991||Aquatechnica, Inc.||Composition and method for purifying water|
|US5076846 *||6 Jun 1990||31 Dic 1991||Pluss-Staufer Ag||Highly concentrated aqueous suspension of minerals and/or fillers and/or pigments, stabilized with one or more polyampholytes|
|US5112782 *||23 May 1991||12 May 1992||Engelhard Corporation||Cationically processed calcined kaolin clay|
|US5126010 *||21 Nov 1990||30 Jun 1992||Oji Paper Co., Ltd.||Ink-jet recording sheet|
|US5147507 *||17 Dic 1990||15 Sep 1992||Pfizer Inc.||Cationic polymer-modified filler material, process for its prepartion and method of its use in papermaking|
|US5244542 *||2 Mar 1992||14 Sep 1993||Ecc International Limited||Aqueous suspensions of calcium-containing fillers|
|US5320773 *||30 Sep 1991||14 Jun 1994||Aquatechnica Inc.||Composition and method for purifying water|
|US5393380 *||18 Ene 1994||28 Feb 1995||Nalco Chemical Company||Polydiallyl dimethyl ammonium chloride/3-acrylamido-3-methylbutanoic acid copolymers and their use for pitch control in paper mill systems|
|US5525296 *||9 Nov 1993||11 Jun 1996||William K. Hollinger, Jr.||Article and method for archival preservation with an organophilic, hydrophobic or acid-resistant molecular sieve|
|US5531821 *||24 Ago 1995||2 Jul 1996||Ecc International Inc.||Surface modified calcium carbonate composition and uses therefor|
|US5584923 *||1 Abr 1996||17 Dic 1996||Ecc International Inc.||Surface modified calcium carbonate composition and uses therefor|
|US5616283 *||25 Ago 1995||1 Abr 1997||Chemical Lime Company||High solids lime as a caustic replacement|
|US5620744 *||4 Ene 1996||15 Abr 1997||Chemical Lime Company||Method of preventing corrosion in concrete pipe|
|US5653795 *||16 Nov 1995||5 Ago 1997||Columbia River Carbonates||Bulking and opacifying fillers for cellulosic products|
|US5676746 *||11 Abr 1995||14 Oct 1997||Columbia River Carbonates||Agglomerates for use in making cellulosic products|
|US5676747 *||29 Dic 1995||14 Oct 1997||Columbia River Carbonates||Calcium carbonate pigments for coating paper and paper board|
|US5676748 *||29 Dic 1995||14 Oct 1997||Columbia River Carbonates||Bulking and opacifying fillers for paper and paper board|
|US5683662 *||5 Jun 1995||4 Nov 1997||Conservation Resources International, Inc.||Article and method for archival preservation with an organophilic, hydrophobic or acid-resistant molecular sieve|
|US5693384 *||16 Mar 1993||2 Dic 1997||Conservation Resources International, Inc.||Article and method for preserving an archival article|
|US5714120 *||5 Jun 1995||3 Feb 1998||Conversation Resources International, Inc.||Method for preserving an archival document or object|
|US5744001 *||19 Feb 1994||28 Abr 1998||Basf Aktiengesellschaft||Aqueous pigment slurries for production of filler-containing paper|
|US5827398 *||13 Feb 1996||27 Oct 1998||Allied Colloids Limited||Production of filled paper|
|US6203722 *||2 Oct 1998||20 Mar 2001||New Eezy Gro, Inc.||Stabilized liquid lime dispersion for sewage treatment|
|US6359040||11 May 1999||19 Mar 2002||Hercules Incorporated||Aqueous systems comprising an ionic polymer and a viscosity promoter, processes for their preparation, and uses thereof|
|US6514384 *||19 Mar 1999||4 Feb 2003||Weyerhaeuser Company||Method for increasing filler retention of cellulosic fiber sheets|
|US6824649||4 Sep 2003||30 Nov 2004||Weyerhaeuser Company||Method for increasing filler retention of cellulosic fiber sheets|
|US6939609 *||12 Mar 1999||6 Sep 2005||Metsä-Serla Oyj||Filler and pigment|
|US7303794||31 Mar 2004||4 Dic 2007||Specialty Minerals (Michigan) Inc.||Ink jet recording paper|
|US7459059||21 Sep 2005||2 Dic 2008||Nalco Company||Use of synthetic metal silicates for increasing retention and drainage during a papermaking process|
|US7476272||29 Nov 2006||13 Ene 2009||E.I. Du Pont De Nemours & Company||Aluminum trihydrate containing slurries|
|US7494565||1 Jun 2006||24 Feb 2009||Nalco Company||Use of starch with synthetic metal silicates for improving a papermaking process|
|US7569148||23 Ago 2007||4 Ago 2009||Siemens Water Technologies Corp.||Continuous membrane filtration and solids reduction|
|US7875213 *||14 Jul 2008||25 Ene 2011||Kemira Oyj||Mineral dispersants and methods for preparing mineral slurries using the same|
|US7931808||9 Jun 2009||26 Abr 2011||Siemens Water Technologies Corp.||Sequencing batch reactor with continuous membrane filtration and solids reduction|
|US8206680||27 Jul 2004||26 Jun 2012||S.A. Lhoist Recherche Et Developpement||Calco-magnesian aqueous suspension and method for the production thereof|
|US9561974 *||17 Ene 2012||7 Feb 2017||Clearflow Group Inc.||Composition and system for flocculating or settling solids from liquids and methods for using same|
|US20030121457 *||31 May 2001||3 Jul 2003||Martin Butters||Stabilised calcium hydroxide slurries|
|US20030136532 *||20 Dic 2002||24 Jul 2003||Weyerhaeuser Company||Method for increasing filler retention of cellulosic fiber sheets|
|US20040045688 *||4 Sep 2003||11 Mar 2004||Weyerhaeuser Company||Method for increasing filler retention of cellulosic fiber sheets|
|US20040133439 *||21 Ago 2003||8 Jul 2004||Dirk Noetzold||Method and system for valuation of complex systems, in particular for corporate rating and valuation|
|US20040150938 *||24 Jul 2003||5 Ago 2004||Illinois Tool Works Inc.||Low voltage modular room ionization system|
|US20050161183 *||21 Ene 2005||28 Jul 2005||Covarrubias Rosa M.||Process for making paper|
|US20050221026 *||31 Mar 2004||6 Oct 2005||Specialty Minerals (Michigan) Inc.||Ink jet recording paper|
|US20060003117 *||14 Jun 2004||5 Ene 2006||Specialty Minerals (Michigan) Inc.||Ink jet recording paper|
|US20060275203 *||27 Jul 2004||7 Dic 2006||Chavez Luis A D||Calco-magnesian aqueous suspension and method for the production thereof|
|US20070036701 *||11 Ago 2005||15 Feb 2007||Huege Fred R||Treatment of high sulfate containing quicklime|
|US20070062659 *||1 Jun 2006||22 Mar 2007||Sherman Laura M||Use of starch with synthetic metal silicates for improving a papermaking process|
|US20070062660 *||21 Sep 2005||22 Mar 2007||Keiser Bruce A||Use of synthetic metal silicates for increasing retention and drainage during a papermaking process|
|US20070068643 *||29 Nov 2006||29 Mar 2007||Defeo Maureen A||Aluminum trihydrate containing slurries|
|US20080206126 *||28 Feb 2007||28 Ago 2008||Robert Benson||Higher than 30% concentration lime slurries, preparation and uses thereof|
|US20090014695 *||14 Jul 2008||15 Ene 2009||Kemira Oyj||Mineral Dispersants and Methods for Preparing Mineral Slurries Using the Same|
|US20090261027 *||9 Jun 2009||22 Oct 2009||Siemens Water Technologies Corp.||Sequencing batch reactor with continuous membrane filtration and solids reduction|
|US20110000403 *||26 Mar 2007||6 Ene 2011||Jean-Yves Tilquin||Stabilization of Milk of Lime Suspensions|
|US20110062377 *||3 Jun 2010||17 Mar 2011||Clearvalue Technologies, Inc.||Clarification of water and wastewater|
|US20130292342 *||17 Ene 2012||7 Nov 2013||Gerald Hanna||Composition and system for flocculating or settling solids from liquids and methods for using same|
|EP1553053A1||5 Dic 1997||13 Jul 2005||Minerals Technologies Inc.||The use of calcium carbonate in an acidic aqueous medium|
|WO1997007882A1 *||23 Ago 1996||6 Mar 1997||Chemical Lime Company||High solids lime as a caustic replacement|
|WO1997041302A1 *||28 Abr 1997||6 Nov 1997||Minerals Technologies Inc.||Rosin-sized paper composition and method of making|
|WO1999002464A1 *||6 Jul 1998||21 Ene 1999||Atlantic Richfield Company||Cement composition containing synthetic hectorite clay|
|WO1999058609A1 *||11 May 1999||18 Nov 1999||Hercules Incorporated||Aqueous systems comprising an ionic polymer and a viscosity promoter|
|WO2001096240A1 *||31 May 2001||20 Dic 2001||Ciba Specialty Chemicals Water Treatments Limited||Stabilised calcium hydroxide slurries|
|WO2004015015A1 *||6 Ago 2003||19 Feb 2004||E.I. Du Pont De Nemours And Company||Aluminum trihydrate containing slurries|
|Clasificación de EE.UU.||252/181, 162/181.1, 162/168.3, 252/175, 162/181.2, 162/181.3|
|Clasificación internacional||C02F1/52, D21H17/67, B01D21/01, C02F1/54, D21H17/69|
|Clasificación cooperativa||C02F1/5236, C02F1/54, D21H17/69, C02F1/5227|
|Clasificación europea||D21H17/69, C02F1/54, C02F1/52F, C02F1/52C|
|23 Dic 1986||CC||Certificate of correction|
|2 Mar 1990||FPAY||Fee payment|
Year of fee payment: 4
|22 Feb 1994||FPAY||Fee payment|
Year of fee payment: 8
|23 Feb 1998||FPAY||Fee payment|
Year of fee payment: 12